Method and device for reducing production of wastewater treatment station sludge with fixed biological cultures

ABSTRACT

The invention concerns a method for reducing production of urban or industrial waste water treatment station sludge with fixed biological cultures. The invention is characterized in that it consists in: dissociating the step of reducing sludge production from the purifying step, by providing a step of activated sludge type biological treatment with low, medium or high load, associated with a sludge production reducing step by thermophilic enzymatic process, or by partial ozone oxidation combined, with mechanical stirring, the substrate source for the biological treatment bacteria consisting of the organic matter derived from lyzed bacterial cells induced during the sludge production reducing step.

The present invention relates to a method and a device for reducing the production of municipal or industrial wastewater treatment station sludge, with fixed biological cultures.

It is known that wastewater purification by the biological method consists in using the organic and nitrogen pollution as a nutrient substrate for the purifying biomass, said carbon and nitrogen pollution being converted to carbon dioxide and to nitrogen, while the biomass proliferates in proportion to the quantity of pollution degraded. The surplus biomass formed constitutes what is commonly referred to as excess biological sludge.

The treatment and final disposal of this sludge is a major environmental and economic challenge. With a forecast annual production, in 2002, of more than 1 200 000 tonnes of dry matter per year for municipal wastewater treatment in France, and more than 10 million tonnes for the European Community, it is clear that the management of the production and treatment of the sludge produced by the purifying stations constitutes a growing preoccupation, amplified by the new regulatory, environmental, health, economic, indeed political and psychological constraints.

Conventional techniques for the disposal of this waste include in particular dumping, agricultural upgrading and incineration. However, these known techniques have serious drawbacks.

Thus the prohibition of dumping of non-ultimate waste, the stringent constraints (especially with respect to heavy metals and certain suspect organic compounds) for agricultural upgrading, the control of the costs and risks of air pollution by incineration, will weigh heavily on the disposal of this waste.

In this context, new technologies have been envisaged, with the aim of reduced sludge production (RSP) from municipal and industrial biological wastewater treatment installations. Some of these RSP techniques are based on the combination of a conventional activated sludge method and a sludge treatment installed in a loop on the aeration tank.

The associated treatment can draw on mechanical, chemical, thermal or biological techniques, and is often based on the combination of two or more of these techniques.

It has been considered to carry out the RSP treatment step by enzymatic degradation (described in particular in EP-A-924 168) or by partial oxidation with ozone combined with mechanical stirring (according to WO 99/06327), installed in parallel and in a loop on the biological tank. These two techniques are highly efficient and, for certain methods, significantly reduce sludge production, by even more than 80%.

FIG. 1 of the appended drawings shows a diagram of a known installation of this type, comprising, in a loop on an aeration tank, a reduced sludge production device which can be an aerobic thermophilic reactor or a partial oxidation unit with ozone producing mechanical stirring. In this figure, the numeral 1 designates the introduction of the wastewater to be treated, which passes respectively through an anaerobic zone R, an anoxic zone X, an aerobic zone A, before being treated in a clarifier C. The RSP reactor, designated as a whole by the letter B, is mounted in parallel and in a loop on the activated sludge treatment installation (C/N/P treatment).

An example of the technical characteristics of such a known installation are given below:

-   -   Equivalent number of inhabitants: 50 000 eq-Hab     -   Daily throughput: 7 500 m³/day     -   Sludge production: 3 000 kg-SM/day     -   Volume of station: 15 000 m³

In this method, a fraction of the sludge present in the aeration tank is sent continuously and possibly after thickening to the reduced sludge production device. Depending on the degree of reduced sludge production required, the quantity of sludge sent daily to the RSP is equivalent to 1 to 10 times the quantity of sludge produced by the water treatment installation in conventional operating conditions. The effluent leaving the RSP loop consists of compounds solubilized in the RSP device and suspended matter. In the example shown in FIG. 1, the installation produces excess sludge of 600 kg SM/d (or 80% RSP).

In the case of biological treatment systems of the “fixed biomass” type, also called “fixed cultures”, the surplus sludge is extracted during the washing and declogging phases. In this case, it is difficult to apply an RSP method in a loop on the water treatment line, particularly for the following reasons:

-   -   The installation of an RSP method in a loop on a fixed biomass         type installation would lead to the reintroduction of a large         quantity of lyzed biomass and SM at the head end of the         installation. This operating mode is not readily compatible with         the load of suspended matter supported by fixed biomass         installations, which is severely limited because of clogging         problems.     -   The excess biomass on fixed biomass biological treatment         installations is extracted in batches during washing phases.         This extraction mode is incompatible with the operating mode of         the RSP loop, which must enable the treatment of a quantity         equivalent to 1 to 10 times the sludge production of the         conventional system.

To solve the problems thus raised by the reduction of sludge production of wastewater treatment stations with fixed biological cultures, the present invention contrasts with the prior art reviewed above, by dissociating the step of reducing sludge production from the purifying step, by providing a step of activated sludge type biological treatment with low, medium or high load, associated with a reduced sludge production (RSP) step by theremophilic enzymatic method, or by partial oxidation with ozone combined with mechanical stirring. The substrate source for the biological treatment bacteria is no longer the organic matter in the wastewater, but the organic matter derived from the lyzed bacterial cells induced during the RSP step.

The present invention further relates to a device for putting into practice the method specified above, in the form of an installation dedicated to reducing sludge production associating an RSP device, with a reactor for biological treatment with low, medium or high load where the substrate source for the bacteria consists of the organic matter derived from the lyzed bacterial cells induced in the RSP reactor.

Other features and advantages of the present invention will appear from the description given below, with reference to the drawings appended hereto which illustrate a non-limiting embodiment. In the drawing:

FIG. 1 illustrates the prior art mentioned above and

FIG. 2 shows the diagram of an installation putting into practice the method of the invention.

Reference to this FIG. 2 shows that this installation is in the form of a platform dedicated to reducing sludge production, which is associated with an installation for wastewater treatment by fixed biomass reactor (for example, biofilter), designated as a whole by the numeral 2. This dedicated platform consists of an RSP device, designated as a whole by the numeral 3, combined with a biological treatment, carried out in a reactor designated by the numeral 8 and comprising a separation-thickening device 9. As shown in this FIG. 2, the organic matter derived from the lyzed bacterial cells induced during the RSP step is the substrate source for the biological treatment in the reactor 8.

Thanks to the invention, it is possible to design a dedicated biological system for reduced sludge production in a very different manner from the wastewater treatment system, allowing a gain in compactness and in efficiency, without having to comply fully with the required treatment constraints for water purification (recycle of the effluent at the front end of the water treatment line, arrow 4).

The cyclic character of the extractions raises no problem for running the RSP device, which can be supplied continuously by withdrawing sludge, after possible thickening, from the separator-thickener 9 of the dedicated system (at 5), the reactor 8 collecting the wash water from the reactor 2. The present invention offers the further advantage of permitting the objective measurement of the reduced quantity of sludge. The reduction in sludge production is calculated from the difference between the quantity of sludge extracted from the water treatment line (at 6) and the quantity of residual sludge extracted (at 7) on the dedicated RSP system.

By way of example, the characteristic data of an embodiment of an installation according to FIG. 2 are given below: Fixed biomass reactor 2 Equivzalent number of inhabitants: 200000 eq-Hab Average daily throughput: 30000 m³/day Sludge production of the 3500 kg SM/day biological treatment stage: Dedicated RSP system 3500 m³/day Daily throughput: Volume of biological treatment: 1200 m³ Volume of enzymatic thermophilic reactor: 650 m³ Sludge production: 350 kg SM/day (90% RSP)

Such a device helps to address the drawbacks of the application, at the fixed biomass biological treatment stations, of the RSP processes directly integrated in a loop. It also provides the following advantages:

-   -   possibility of adjusting sludge reduction as required (20 to         100% reduction);     -   possibility of treating biofilter wash water;     -   possibility of designing a biological sludge reduction device         for a purification level much lower than the purification level         required for actual wastewater treatment;     -   dimensioning of the RSP device for a hydraulic throughput 5 to         50 times lower than the throughput of the purification station         that generated the sludge; and     -   possibility of adapting the oxygenation capacity and the air or         oxygen diffusion mode independently of that of the station that         generated the sludge.

It is obviously understood that the present invention is not limited to the embodiment described and shown here, but includes all possible variants thereof. 

1. A method for reducing the production of municipal or industrial wastewater treatment station sludge, with fixed biological cultures, characterized in that it consists in dissociating the step of reducing sludge production from the purifying step, by providing a step of activated sludge type biological treatment with low, medium or high load, associated with a reduced sludge production (RSP) step by theremophilic enzymatic method, or by partial oxidation with ozone combined with mechanical stirring, the substrate source for the biological treatment bacteria consisting of the organic matter derived from lyzed bacterial cells induced during the reduced sludge production (RSP) step.
 2. A device for putting into practice the method as claimed in claim 1, characterized in that it is in the form of an installation dedicated to reducing sludge production associating an RSP device (3), with a reactor for biological treatment with low, medium or high load (8) whereof the substrate source for the bacteria consists of the organic matter derived from the lyzed bacterial cells induced by the reduced sludge production device (3).
 3. The device as claimed in claim 2, characterized in that the RSP device (3) is supplied continuously by withdrawing sludge after possible thickening in the separator-thickener (9) collecting the activated sludge leaving the biological treatment reactor (8). 